[0001] The present invention relates to the preparaton of novel modified polymer polyols
and their use in making polyurethane foam. In particular, the present invention relates
to the preparation of polymer polyols suitable for use in the manufacture of polyurethane
foams which are fire resistant.
[0002] It is known to prepare polyurethane foams having improved fire resistant properties
relative to conventional foams. Such improved fire resistant properties are usually
achieved by adding a flame retardant directly into the polyurethane foam formulation
along with the other components. Whilst such a method is applicable to flame retardants
which are either liquids or solids which are soluble in the foam formulation, it is
not generally suitable where the flame retardant is a solid which is insoluble in
the foam formulation as it is difficult to achieve homogenous dispersion of the flame
retardant.
[0003] An approach to rednering polyurethane foams fire resistant has now been developed
which allows a wider range of flame retardants to be used than before. The approach,
which in particular relates to polyurethane foams derived from so-called polymer polyols
or graft polyols, comprises incorporating the flame retardant into the polymer polyol
during the polymer polyol production stage. Surprisingly, it has been observed that,
by using such an approach, it is possible to carry out incorporation of the flame
retardant without seriously effecting the viscosity and stability of the polymer polyol.
[0004] The approach described above is especially suitable when solid flame retardants are
used, since by this method the flame retardant can be incorporated relatively homogenously
into the polymer polyol and hence the foam formulation. As a consequence not only
is the fire resistance improved for a given level of flame retardant but it has also
been found that the quality of the foam structure is improved. The latter effect is
also true if liquid retardants are incorporated during the polymer polyol production
stage.
[0005] Accordingly, the present invention provides a fluid polymer polyol dispersion prepared
by reacting a polyol with one or more monomers and an effective amount of a free radical
polymerisation catalyst under conditions where the monomer is grafted onto the polyol
characterised in that the reaction is carried out in the presence of between 1 and
300/0 by weight of a flame retardant.
[0006] As regards the polyol used in preparing the fluid polymer polyol dispersion, this
is conveniently a polyether polyol and is optionally one with deliberately added unsaturation,
as might be introduced, for example, by reaction of a polyol with an unsaturated anhydride
such as maleic anhydride or the stabilisers of EP 162588 and EP 162589. Typical polyols
which are contemplated by this invention are alkylene oxide adducts of (1) low molecular
weight diols and triols or naturally occuring polyols (2) non reducing sugars and
derivatives thereof (3) phosphoric, phosphorus, and polyphosphoric acids. Examples
of such adducts are the alkylene oxide adducts of ethylene glycol, propylene glycol,
glycerol, trimethylolpropane, the isomeric butanediols, hexanediols, octanediols and
the like. Alkylene oxide adducts of pentaerythritol, sorbitol, arabitol, mannitol,
alkyl glucoside, alkylene glycol glucosides and glycerol glucosides are also contemplated,
as are adducts of alkylene diamines and hydrazine.
[0007] In general it is desirable that the alkylene oxide used to form the adduct is a 1,2
or 1,3 or 1,4 alkylene oxide having from 2 to 4 carbon atoms. Preferred examples are
ethylene oxide, propylene oxide, the butylene oxides, THF, or mixtures thereof, with
ethylene oxide and/or propylene oxide being the most preferred.
[0008] With such a large number of polyols available for use with the above invention, the
choice of polyol will depend very much upon the application for which the polymer
polyol is used. In choosing the polyol, an important consideration is its hydroxyl
number, that is the average number of free hydroxyl groups per polyol molecule, since
this reflects the number of sites available, on the polyol for reaction with isocyanate.
Broadly speaking, the larger the hydroxyl number of the polyol the more sites available
for participation in the urethane linkage forming reaction and hence the more rigid
the foam or elastomer formed. The hydroxyl number of the polyol is conveniently between
10 to 600 and preferably between 20 and 70.
[0009] The polyols should have viscosities in the range 10-2,000 Kgm-'s-
1 centipoise at 25°C, preferably in the range 10-300 Kgm-Is-
1.
[0010] The monomer used is preferably a vinyl monomer. Suitable vinyl monomers inlcude styrene,
acrylonitrile, methacrylonitrile and methylmethacrylate. Under the reactions conditions
monomer is grafted onto the backbone by afree radical polymerisation process to produce
grafted polymer moieties. It is preferred that the process employs a monomer mixture
comprising styrene and acrylonitrile thereby producing a styrene/acrylonitrile copolymer
grafted polyol. In this latter case, the ratio of styrene to acrylonitrile can be
varied from a ratio producing essentially pure polystyrene through a range of intermediate
copolymers to one producing essentially pure polyacrylonitrile. However in general
it is desirable to use as much of the cheaper styrene as possible consistent with
producing polymer polyols of the correct viscosity and stability which do not give
rise to scorch in the final polyurethane foam. A preferred range of styrene acrylonitrile
weight ratios is 3:1 to 1:2. The monomer or monomers used in the present invention
are grafted and polymerised by means of a free radical polymerisation catalyst which
is added in catalytic amounts to the polyol/monomer mixture. Such catalysts include
for example peroxides, e.g hydrogen peroxide, di-t-butyl peroxide, dibenzoylperoxide
t-butylhydroperoxide; azo compounds such a azobisisobutyronitrile; as well as persulphates,
perborates, percarbonates and the like.
[0011] Although the flame retardant can be in principle any material which will improve
the fire resistance of polymers the preferred compounds are ones containing phosphorus.
Preferably, such phosphorus containing compounds are phosphines, phosphites or phosphates
which are substituted with an aryl radical or a halogenated hydrocarbyl radical. Examples
of such phosphorus containing compounds include triphenylphosphine, triphenylphosphate,
1,2-diphenylphosphinoethane, triaryl phosphate esters of the type described in EP170206,
diphenylphosphate, 2-ethylhexyl, diphenylphosphate, tetrakis (2-chloroethyl)ethylenediphosphate
and the like.
[0012] The preparation of the fluid polymer polyol dispersion is suitably carried out by
reacting the polyol, monomers(s), polymerisation catalyst and flame retardant at a
temperature such that the half-life of the polymerisation catalyst is less than six
minutes. In practical terms this usually means a temperature in the range 60-150°
C preferably 80-125° C.
[0013] The process can be carried out for example by feeding the reactants to a continuously
operated stirred reaction vessel operating at an appropriate temperature. The extent
of polymerisation and grafting can be controlled by choosing an appropriate residence
time for the reactants.
[0014] In preparing the fluid polymer polyol dispersion, the reactants are suitably employed
in amounts such that the reaction mixture comprises between 5 and 50% preferably between
10 and 400/0 by weight monomer(s) and between 1 and 30% preferably 2 and 5
0/
0 by weight flame retardant with the balance comprising polyol, polymerisation catalyst
and optional extras such as solvents, stabilisers and the like.
[0015] The fluid polymer dispersions of the present invention are useful in producing polyurethane
foam having improved fire resistance. Accordingly there is also provided a process
for producing polyurethane foam which comprises reacting and foaming (a) a fluid polymer
polyol dispersion of the type described herein (b) an organic polyfunctional isocyanate,
(c) a catalyst for the reaction of components (a) and (b) and (d) a blowing agent.
[0016] Techniques for formulating such mixtures are well known to those in the art and include
for example one-shot methods performed at or about room temperature.
[0017] Organic polyfunctional isocyanates which can be used in the preparation of polyurethane
foam will be known to the skilled man. Preferred organic polyfunctional isocyanates
include the isomers of toluene diisocyanate (TDI), di(4-isocyantophenyl) methane (MDI)
and derivatives as well as C
2-Cio alkylene diisocyanates and prepolymers of such compounds.
[0018] Catalysts which can be used in producing polyurethane foams include teriary amines
and phosphines, strong inorganic bases such as alkali metal hydroxides and alkoxides
and carboxylates of tin, titanium and aluminium.
[0019] As regards the blowing agent, this preferably water but halogenated hydrocarbons,
e.g. dichloromethane, 1,1-dichloro-1-fluoromethane and the like, nitrogen, air and
carbon dioxide can also be used.
[0020] Other additives in addition to the above can be employed e.g. foam stabilisers, pigments,
fillers and the like can also be used. Such optional additives will be familiar to
the skilled man.
[0021] The invention is now illustrated by the following Examples.
Example 1 - Preparation of a flame retardant polymer polyol using triphenylphosphine
[0022] 62.5g of triphenylphoshine, 201g of styrene and 86.3g of acrylonitrile were mixed
until a clear solution was formed. To this mixture was added 4.4g of the polymerisation
catalyst azobisisobutyronitrile (AIBN), 62.5g of stabiliser polyol RP 1268 (stabiliser
according to EP 162589) and 277g of polyol CP3 (ex BP Chemicals Ltd). The above premix
was added into 555g of a polyether triol (MW = 4800) over 30 minutes at 12°C. After
addition the total mixture was maintained at 125° C for a further 30 minutes before
it was cooled. After cooling volatiles were stripped in a Buchi evaporator over 90
minutes.
[0023] The product which comprised a flame retardant polymer had the following properties:
viscosity = 216 Kgm-1s-1
centrifugal solids = 1.6%
polymer content - 230/0
filtrability - 150 mesh (17 secs) 100%
700 mesh (150 secs) 650/0
Example 2 - Preparation of polurethane foam from the polymer polyol of Example 1
[0024] A polyurethane foam was produced from a formulation having the composition:
[0025] The polyurethane foam had a density of 45gi-
1.
Comparative Test A
[0026] A polymer polyol was prepared exactly as according to Example 1 except that the triphenylphosphine
was omitted. The polymer polyol produced was added to the polurethane foam formulation
of Example 2 together with 3.75 parts by weight triphenylphosphine. The final foam
had a density of 46gi-
1.
Flammability Test
[0027] 5 pieces of the Example 2 polyurethane foam and 5 pieces of the comparative test
foam, each piece being of dimensions 30 x 7.5 x 1.25 cm, was submitted to the California
Test 117A for flammability. The results were as follows:
[0028] These results show that polyurethane foams made from the polyols of the present invention
char less and flame for a shorter time relative to those foams prepared by adding
the flame retardant into the foam formulation.
Comparative Test B
[0029] Comparative Test A was repeated except that the triphenylphosphine was completely
omitted. The foam produced had a density of 45.4gl-
1.
[0030] The results of the flammability test (averaged over 5 pieces) were:
Average Char length : 300 mm
Average after flame time : 45.3
Example 3 - Preparation of a flame retardant polymer polyol using triphenylphosphate
[0031] Example 1 was repeated except that triphenylphosphate was used in place of triphenylphosphine.
The product polymer polyol had the following properties:
viscosity = 237 Kgm-1s-1
centrifugal solids =1.7%
polymer content =23%
filtrability = 150 mesh (17 seconds) 100%
700 mesh (150 seconds) 66%
Example 4 - Preparation of polyurethane foam and flammability test
[0032] A polyurethane foam was prepared from the polymer polyol of Example 3 using the formulation
of Example 2. The foam had a density of 45gl-
1. The results of the flammability test (averaged over 5 pieces) were as follows: Average
Char length : 35.6mm Average after flame time : 0 secs
[0033] Example 5 - Preparation of polymer polyol using tetrakis (2-chloroethyl) ethylene
diphosphate
[0034] Example 1 was repeated except that the above-mentioned phosphate was used in place
of triphenylphosphine. The product polymer polyol had the following properties:
viscosity = 239 Kgm-1s-1
centrifugal solids = 1.6%
polymer content - 23%
filtrability = 150 mesh (17 seconds) 100%
700 mesh (150 seconds) 72%
Example 6 - Preparation of polyurethane foam and flammability test
[0035] A polyurethane foam was prepared from the polymer polyol of Example 5 using the formulation
of Example 2. The results of the flammability test (averaged over 5 pieces) were as
follows: Average char length : 52.2mm Average after flame time : 0 secs To summarise,
the Examples and Comparative Tests show that, when fluid polymer polyol dispersions
of the present invention are used, the flame resistance of the resulting polyurethane
foam is better than observed (a) when unmodified polymer polyol dispersions alone
are used or (b) when unmodified polymer polyol dispersions are used in conjunction
with a flame retardant added separately to the polyurethane foam formulation.
1. A fluid polymer polyol dispersion prepared by reacting a polyol with one or more
monomers and an effective amount of a free radical polymerisation catalyst under conditions
where monomer is grafted onto the polyol characterised in that the reaction is carried
out in the presence of between 1 and 300/0 by weight of a flame retardant.
2. A fluid polymer polyol dispersion as claimed in claim 1 characterised in that the
reaction is carried out in the presence of between 2 and 5% by weight of the flame
retardant.
3. A fluid polymer polymer polyol dispersion as claimed in claim 1 characterised in
that the flame retardant is selected from triphenylphosphine, triphenylphosphate,
triarylphosphate esters, diphenylphospate 2-ethylhexyl, diphenylphospate and tetrakis
(2-chloroethyl)ethylenediphosphate.
4. A fluid polymer polyol dispersion as claimed in claim 3 characterised in that the
monomer(s) used in the reaction are selected from styrene, acrylonitrile or mixtures
thereof.
5. A process for preparing polyurethane foam which comprises reacting and foaming
a formulation characterised in that the formulation comprises (a) a fluid polymer
polyol dispersion of the type defined in claim 1; (b) an organic polyfunctional isocyanate;
(c) a catalyst for the reaction of components (a) and (b) and (d) a blowing agent.